US4162958A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Process for the discharge of ash concentrate from a coal deashing system
Assignee: Kerr McGee Corp
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Filing: 1978-03-20
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Granted: 1979-07-31
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Expires: 1998-03-20
Abstract
Abstract An improved process for the continuous discharge from a first separation zone of a first heavy fraction comprising insoluble coal products and solvent in a coal deashing process utilizing solvents at elevated pressures and temperatures near the critical temperature of the solvent. The continuous discharge of the insoluble coal products in a dry, powdery form, is achieved by monitoring the temperature level of the solvent and insoluble coal products within a transfer conduit after withdrawal and pressure reduction from the first separation zone operating pressure, at a temperature below about 550 degrees F.
Inventors
- 👤 Roger A. Baldwin
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-31 10:43
CPC Classifications
C; C10; C10G; C10G1/00; C10G1/04; C10G1/045
Claims Analysis
Total Claims: 6
Claim 1
Independent Claim
246 words
In a process for separating a feed mixture comprising soluble coal products, insoluble coal products and a solvent in a separation zone, said solvent consisting essentially of at least one substance having a critical temperature below 800 degrees F. selected from the group consisting of aromatic hydrocarbons having a single benzene nucleus and normal boiling points below about 310 degrees F., cycloparaffin hydrocarbons having normal boiling points below about 310 degrees F., open chain mono-olefin hydrocarbons having normal boiling points below about 310 degrees F., open chain saturated hydrocarbons having normal boiling points below about 310 degrees F., mono-, di, and tri-open chain amines containing from about 2-8 carbon atoms, carbocyclic amines having a monocyclic structure containing from about 6-9 carbon atoms, heterocyclic amines containing from about 5-9 carbon atoms, and phenols containing from about 6-9 carbon atoms and their homologs, in which said feed mixture is maintained in said separation zone at an elevated temperature and pressure to separate said feed mixture into a light fraction and into a heavy fraction comprising insoluble coal products and some solvent and in which withdrawing said heavy fraction from said separation zone and reducing the pressure level of said heavy fraction at least about 100 psig fails to yield a dry, powdery, ash concentrate composition, the improvement which comprises: reducing the temperature level of the heavy fraction after pressure reduction to a temperature level below about 550 degrees F. to continuously yield a dry, powdery, ash concentrate composition.
Claim 2
Dependent Claim
246 words
In a process for separating a feed mixture comprising soluble coal products, insoluble coal products and a solvent in a separation zone, said solvent consisting essentially of at least one substance having a critical temperature below 800 degrees F. selected from the group consisting of aromatic hydrocarbons having a single benzene nucleus and normal boiling points below about 310 degrees F., cycloparaffin hydrocarbons having normal boiling points below about 310 degrees F., open chain mono-olefin hydrocarbons having normal boiling points below about 310 degrees F., open chain saturated hydrocarbons having normal boiling points below about 310 degrees F., mono-, di, and tri-open chain amines containing from about 2-8 carbon atoms, carbocyclic amines having a monocyclic structure containing from about 6-9 carbon atoms, heterocyclic amines containing from about 5-9 carbon atoms, and phenols containing from about 6-9 carbon atoms and their homologs, in which said feed mixture is maintained in said separation zone at an elevated temperature and pressure to separate said feed mixture into a light fraction and into a heavy fraction comprising insoluble coal products and some solvent and in which withdrawing said heavy fraction from said separation zone and reducing the pressure level of said heavy fraction at least about 100 psig fails to yield a dry, powdery, ash concentrate composition, the improvement which comprises: reducing the temperature level of the heavy fraction after pressure reduction to a temperature level below about 550 degrees F. to continuously yield a dry, powdery, ash concentrate composition.
Claim 3
Dependent Claim
48 words
The process of claim 1 wherein the elevated temperature and pressure is defined further as: a temperature level in the range of from about 400 degrees F. to about 700 degrees F. and a pressure level in the range of from about 700 psig to about 1000 psig.
Claim 4
Dependent Claim
31 words
The process of claim 2 wherein the temperature level is defined further as: preferably a temperature level in the range of from about 400 degrees F. to about 650 degrees F.
Claim 5
Dependent Claim
27 words
The process of claim 1 wherein the pressure reduction is defined further as: preferably reducing the pressure level of the heavy fraction at least about 500 psig.
Claim 6
Dependent Claim
49 words
The process of claim 1 wherein reducing the temperature level of the heavy fraction after pressure reduction is defined further as: reducing the temperature level of the heavy fraction through controlled flash cooling of the heavy fraction during pressure reduction to a temperature level below about 550 degrees F.
References Cited (Backward Citations)
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1982-07-30 | 1983-01-29 | 1983-07-31 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1986-07-30 | 1987-01-29 | 1987-07-31 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1990-07-30 | 1991-01-29 | 1991-07-31 | $7700.00 | Window Closed / Lapsed |